US6139313A - Furnace having toroidal fluid flow heating zone - Google Patents

Furnace having toroidal fluid flow heating zone Download PDF

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Publication number
US6139313A
US6139313A US09/214,951 US21495199A US6139313A US 6139313 A US6139313 A US 6139313A US 21495199 A US21495199 A US 21495199A US 6139313 A US6139313 A US 6139313A
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Prior art keywords
furnace
chamber
fuel
fluid
ring
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US09/214,951
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English (en)
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Jacek Antoni Kostuch
Christopher Edward Dodson
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Mortimer Technology Holdings Ltd
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Mortimer Technology Holdings Ltd
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Priority claimed from GB9615425A external-priority patent/GB2315432B/en
Priority claimed from GB9615418A external-priority patent/GB2315431B/en
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Assigned to MORTIMER TECHNOLOGY HOLDINGS LIMITED reassignment MORTIMER TECHNOLOGY HOLDINGS LIMITED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: DODSON, CHRISTOPHER EDWARD, KOSTUCH, JACEK ANTONI
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/24—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique
    • B01J8/38—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it
    • B01J8/384—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only
    • B01J8/386—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles according to "fluidised-bed" technique with fluidised bed containing a rotatable device or being subject to rotation or to a circulatory movement, i.e. leaving a vessel and subsequently re-entering it being subject to a circulatory movement only internally, i.e. the particles rotate within the vessel
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J6/00—Heat treatments such as Calcining; Fusing ; Pyrolysis
    • B01J6/001—Calcining
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/18—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with fluidised particles
    • B01J8/1836—Heating and cooling the reactor
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00—Fluidised bed combustion apparatus
    • F23C10/18—Details; Accessories
    • F23C10/20—Inlets for fluidisation air, e.g. grids; Bottoms
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23C—METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN  A CARRIER GAS OR AIR 
    • F23C10/00—Fluidised bed combustion apparatus
    • F23C10/18—Details; Accessories
    • F23C10/22—Fuel feeders specially adapted for fluidised bed combustion apparatus
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
    • F27B15/10—Arrangements of air or gas supply devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
    • F27B15/14—Arrangements of heating devices
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27—FURNACES; KILNS; OVENS; RETORTS
    • F27B—FURNACES, KILNS, OVENS, OR RETORTS IN GENERAL; OPEN SINTERING OR LIKE APPARATUS
    • F27B15/00—Fluidised-bed furnaces; Other furnaces using or treating finely-divided materials in dispersion
    • F27B15/02—Details, accessories, or equipment peculiar to furnaces of these types
    • F27B15/16—Arrangements of cooling devices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00044—Temperature measurement
    • B01J2208/00061—Temperature measurement of the reactants
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00026—Controlling or regulating the heat exchange system
    • B01J2208/00035—Controlling or regulating the heat exchange system involving measured parameters
    • B01J2208/00088—Flow rate measurement
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00106—Controlling the temperature by indirect heat exchange
    • B01J2208/00265—Part of all of the reactants being heated or cooled outside the reactor while recycling
    • B01J2208/00274—Part of all of the reactants being heated or cooled outside the reactor while recycling involving reactant vapours
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/00353—Non-cryogenic fluids
    • B01J2208/00371—Non-cryogenic fluids gaseous
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00327—Controlling the temperature by direct heat exchange
    • B01J2208/00336—Controlling the temperature by direct heat exchange adding a temperature modifying medium to the reactants
    • B01J2208/0038—Solids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00477—Controlling the temperature by thermal insulation means
    • B01J2208/00495—Controlling the temperature by thermal insulation means using insulating materials or refractories
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/0053—Controlling multiple zones along the direction of flow, e.g. pre-heating and after-cooling

Definitions

  • the present invention relates to furnaces.
  • it relates to furnaces of the kind in which a toroidal fluid flow heating zone is established.
  • Such furnaces are described, for example, in U.S. Pat. No. 4,479,920.
  • a hot gas is passed through gaps between angled blades or vanes in a ring of blades or vanes provided in an operational chamber of the furnace.
  • the blade ring is formed in an annular gap between the wall of the chamber and a central block, for example, an upwardly pointing conical portion, located on the axis of the chamber.
  • Gas flow is caused to follow a rotary path in a doughnut shaped region around the block and in individual swirls within the rotary path. This ensures efficient residence of, and heat transfer to, material, such as particulate material, to be heated in the gas flow.
  • Furnaces of the said kind may be used for the heat treatment of particulate material.
  • the feed particulate material comprises material which fluxes at temperatures at which it is to be heat treated
  • unwanted build up of the fluxed material occurs in various parts of the furnace, especially on or around the ring of angled blades and on or around the central block.
  • such build up can cause a back pressure to occur which impedes the particulate feed system and/or extinguishes the burner employed to provide the hot gas.
  • build-up of material requires removal before the furnace can be suitably operated again. This necessitates terminating the use of the furnace and undesirably limits the duration of that use.
  • Such limitations make prior art furnaces of the above kind unsuitable for some continuous heat treatment processes.
  • a furnace of the kind in which a toroidal fluid flow heating zone may be established including a chamber in which there is provided an inner block, and a ring of angled blades between the inner block and an inner wall of the chamber; means for delivering fluid into the chamber in such a way that the fluid passes through gaps between the blades and establishes a toroidal fluid flow heating zone in the chamber above the ring of angled blades; means for injecting feed particulate material into the chamber in a region where the toroidal fluid flow is to be established; and means for injecting fuel into the chamber in a region above the ring of angled blades such that the region in the chamber at which the heating zone in the chamber is established is elevated above the ring of angled blades.
  • the fuel injected by such means may be reacted with a reacting fluid delivered into the chamber in the usual manner through the gaps between the angled blades.
  • the fuel may be a combustible fuel and the reacting fluid may be air or an oxygen containing fluid, whereby, if sufficient oxygen is available at a suitable elevated temperature, spontaneous reaction of the fuel and oxygen takes place to provide the required heating zone.
  • This may constitute a plasma in part of, for example, in the upper part of, the toroidal flow.
  • One advantage of this aspect of the present invention is that the delivery of excessively hot gas to the operational chamber via the ring of angled blades can be avoided. This avoids damage to the ring of angled blades and neighbouring components and also avoids unwanted accretion of material being processed on the hot surfaces.
  • the energy demands of the furnace are considerably raised and hot gas at a temperature as high as 1600° C. to 1700° C. might need to be delivered via the ring of angled blades. Such high temperatures can cause damage to the ring.
  • the reacting fluid may be delivered at a temperature in the range from 700° C. to 900° C., and especially from 700° C. to 800° C. to provide a heating zone temperature of from 750° C. to 1050° C., for example 920° C. to 1020° C.
  • the means for injecting fuel may comprise a ring of fuel inlet tubes extending from a common joint or housing to which input fuel is applied via an inlet pipe, the inlet tubes ending in the operational chamber.
  • the tubes are upwardly pointed at their ends in the chamber thereby providing jets of fuel which are injected into the main fluid flow to provide combustion to form the required heating zone by, for example, the said plasma.
  • the main fluid flow may comprise air which is preheated before delivery into the operational chamber through the gaps in the ring of angled blades.
  • the heated air flow may be provided by combining with an excess supply of air a burning pre-heating fuel and exhaust gases produced by burning the pre-heating fuel.
  • the fuel which may be employed to provide pre-heating of the air flow and the fuel which may be injected directly into the operational chamber in the furnace may be the same or different fuels.
  • the two fuels are the same.
  • the fuel employed in the operation of the furnace may be natural gas. It could alternatively comprise fuel oil, pulverised coal, or combustibles obtained from lignitic materials.
  • the temperature inside the operational chamber may be monitored.
  • the rate of delivery of the fuel and/or the reacting fluid may be controlled by adjustment according to variations of the monitored temperature from a desired norm representing the required heating zone temperature.
  • the feed material may comprise a particulate material of a kind which fluxes at temperatures above about 800° C.
  • the feed material may comprise mineral particles, for example, clays such as kaolin, calcium carbonate or mica to be flash calcined using the furnace.
  • the furnace way be adjusted so that the temperature of calcination is in the range from 750° C. to 1050° C., for example, from 920° C. to 1020° C.
  • the application of fuel through a further inlet means allows the heating zone provided by the toroidal fluid flow to be moved upwardly away from the ring of blades and the region of the chamber wall and the inner block immediately above the ring of blades thereby preventing overheating of the surfaces of these members.
  • a furnace of the kind in which a toroidal fluid flow heating zone may be established including a chamber in which there is provided an inner block, and a ring of angled blades between the inner block and an inner wall of the chamber; means for delivering fluid into the chamber in such a way that the fluid passes through gaps between the blades and establishes a toroidal fluid flow heating zone in the chamber above the ring of angled blades; means for injecting feed particulate material into the chamber in a region where the toroidal fluid flow is to be established; and means for cooling the inner block.
  • the means for cooling the block may conveniently comprise a radiation heat shield in the form of a shroud provided over the inner block.
  • the means for delivering coolant gas may comprise a gas inlet pipe or pipes extending from a region outside the furnace to the shroud.
  • the gas inlet pipe(s) may extend from a region above or below or to the side of the shroud.
  • the coolant gas may, for example, comprise air.
  • the inner block may, as in the prior art, comprise a portion whose cross-sectional area decreases along its axis in a direction away from the ring of angled blades.
  • the block may comprise an upwardly pointing conical or frusto-conical portion.
  • the portion may be made of refractory material.
  • the shroud may comprise a cover of similar shape, for example, an upwardly pointing frusto-conical portion spaced from the block.
  • the means for delivering coolant gas to the shroud may include a coolant gas delivery pipe extending downwardly to the top of the shroud, for example, from the top of the furnace or extending upwardly, for example, from the bottom of the furnace.
  • the chamber may have a wall having a frusto-conical portion which is connected at its narrower end to a product outlet pipe.
  • the furnace according to the second aspect of the present invention beneficially prevents overheating occurring at the inner block.
  • the shroud provides a radiation heat shield for the inner block and also allows cooling of the inner block by delivery of coolant gas for application over the surface of the inner block.
  • the coolant gas such as air, provides an insulating layer between the shroud, which may be made, for example, of stainless steel, and the inner block, which may be made, for example, of stainless steel or of refractory material.
  • the coolant gas also serves to remove any conducted heat from the shroud thus improving its function as a radiation shield.
  • the operational chamber enclosure may lead to a product exit chamber and may be provided with a conical shape having a smooth profile with no internal ledges or low velocity zones which facilitates transfer of product material after heat treatment in the operational chamber of the furnace without significant accretion on the walls.
  • FIG. 1 is a cross-sectional side elevation of a prior art furnace of the kind producing a toroidal fluid flow heating zone
  • FIG. 2 is a cross-sectional side elevation of a furnace of the kind producing a toroidal fluid flow heating zone and embodying the present invention.
  • FIG. 1 A prior art furnace having a fluid flow heating zone of the toroidal kind is shown in FIG. 1.
  • An enclosure 1 has a top 2, a base 3 and a side wall 4.
  • a structure 5 made of refractory material comprising stacked annular portions 5a, 5b, 5c, 5d and 5e is supported by the base 3.
  • An annular refractory portion 6 is provided between the portions 5a and 5b and an annular refractory portion 8 is provided between the portions 5a, 5b and 5c and covers an opening 4a in the side wall 4 whereby a passage 7 is provided inside the structure 5, the passage 7 communicating with a pipe 9 fitted to the side wall 4 at the opening 4a.
  • a tubular support 11 extends upwardly from the portion 6 through the passage 7.
  • the support 11 carries a frusto-conical refractory portion 13 having an internal axial bore 14 and a refractory portion 15 located on top of the portion 13 by a portion 15a which engages within the top of the bore 14.
  • a support 17 is attached to the tubular support 11 near its upper end and to a flange 19 extending into the passage 7 from the portion 5c.
  • a ring 21 of angled blades is provided in the narrow gap between the lower end of the portion 13 and the outer portion 5d. The blades are of the form described in U.S. Pat. No. 4,479,920. The ring 21 is supported between the portion 5d and the support 17.
  • the uppermost refractory portion 5e in the structure 5 is fitted to an outlet chamber 25 whereby the chamber 7a communicates with the outlet chamber 25.
  • An outlet pipe 28 extends from the outlet chamber 25.
  • An inlet pipe 27 extends from the top 2 of the enclosure 1 through the chamber 25 and extends into the chamber 7a.
  • hot gas from a burner (not shown) at a temperature required to establish heating in the chamber 7a is delivered into the passage 7 via the pipe 9.
  • the gas passes through the gaps between the blades of the ring 21.
  • a toroidal hot gas flow is thereby established near the ring 21 in the chamber 7a.
  • Material to be heat treated in the furnace is introduced via the inlet pipe 27 into the heating zone provided by the toroidal flow.
  • the powdered product formed by this process is eventually (after a residence time typically of a few seconds in the heating zone) transferred into the chamber 25 from the chamber 7a and is extracted by a cyclone (not shown) attached to the outlet pipe 28 where product solid material is separated from output gases.
  • FIG. 2 shows a furnace embodying the present invention for producing a fluid flow heating zone of the toroidal kind.
  • items which are similar to items in the furnace shown in FIG. 1 have been accorded like reference numerals.
  • an inverted conical shroud 31 is provided to cover the conical refractory portion 15 and part of the surface of the portion 13 below it.
  • An inlet tube 33 extends downwardly along the axis of the enclosure 1 and enters the shroud 31.
  • the uppermost portion 5e is shortened and a conical enclosure wall 35 extending from the top of the portion 5e is formed around the upper chamber 7a.
  • the upper end of the enclosure wall 35 has a tubular neck 35a which is fitted through the top 2 of the enclosure 1 into a tubular connector 37 outside the enclosure 1.
  • An outlet pipe 39 is also fitted into the connector 37.
  • the pipe 39 leads to a cyclone 41.
  • the upper part of the inlet tube 33 extends through the interior of part of the pipe 39, and the connector 37 and the neck 35a into the conical enclosure 35.
  • the portion 13 in FIG. 2 has no bore and is supported by blocks 42, 43 which are stainless steel support rings provided between the support 17 and portion 13.
  • a ring of fuel inlet tubes 45 (of which only two are shown in FIG. 2) is provided beneath the blocks 42, 43.
  • the tubes 45 project upwardly at their inner ends into the chamber 7a above the ring 21.
  • the tubes 45 are connected at a central joint 47 to which in turn is connected a single inlet pipe 49 extending through the base 3, portion 6 and tubular support 11.
  • a series of feed material inlet tubes 23 (only one of which is shown) is provided.
  • the tubes 23 are spaced circumferentially around the wall 4 and are fitted through the wall 4 and the portion 5d to enter the chamber 7a.
  • reacting fluid for example, hot air
  • reacting fluid for example, hot air
  • the air may be heated by burning fuel in a burner (not shown) and allowing the burning fuel and hot exhaust gases produced thereby to be combined with the air flow to be heated.
  • the hot fluid passes through the gaps between blades of the ring 21 and thereby forms a toroidal flow above the ring 21.
  • Fuel is delivered along the inlet pipe 49 and is injected as jets into the chamber 7a via the connector 47 and tubes 45.
  • the fuel undergoes a spontaneous reaction with the reacting fluid in the chamber 7a thereby providing a plasma heating zone in the toroidal flow.
  • This causes the location in the chamber 7a at which the heating zone is established to be elevated to a region clear of the narrow gap between the portion 5d and the base of the portion 13 and the blocks 42 and 43 thereby avoiding overheating of the blades of the ring 21 and the surfaces adjacent to the ring 21.
  • the reacting fluid is delivered at a temperature of, for example, 750° C. to 800° C. less than the 1500° C. to 1600° C. required in some processes by the use of the furnace of FIG. 1.
  • the fuel used to preheat the reacting fluid may be the same as the fuel delivered into the chamber 7a via the tubes 45 and may, for example, comprise natural gas.
  • Particulate material is injected via the inlet tubes 23 into the plasma heating zone established in the toroidal flow. Coolant gas is delivered down the inlet pipe 33 to the shroud 31 and is applied over the surface of the portion 15 and part of the portion 13. The coolant gas prevents overheating of the portions 13 and 15 and also of the shroud 31 and thereby eliminates a local hot surface on the block 15 on which accretion of particulate material can occur.
  • the treated particulate material after a suitable residence in the chamber 7a, which is typically less than 0.1 seconds, is drawn upwardly through the conical enclosure 35 and into the outlet pipe 39. This product is extracted and separated from the gas stream containing it by the cyclone 41.
  • heat treatment processes may be operated using the furnace shown in FIG. 2 in a continuous manner without the need for frequent cleaning of deposited material from inside the chambers of the furnace as with the prior art furnace of FIG. 1.
  • the temperature in the chamber 7a enclosed by the enclosure wall 35 may be monitored by, for example, a thermocouple (not shown), fitted to the inside of the wall 35, and variations of the temperature from a suitable norm may be employed as control signals to adjust the rate of delivery of fuel to the chamber via the fuel inlet tubes 45.
  • a thermocouple (not shown) fitted to the inside of the wall 35, and variations of the temperature from a suitable norm may be employed as control signals to adjust the rate of delivery of fuel to the chamber via the fuel inlet tubes 45.

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Dispersion Chemistry (AREA)
  • Combustion & Propulsion (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Furnace Details (AREA)
  • Feeding, Discharge, Calcimining, Fusing, And Gas-Generation Devices (AREA)
  • Drying Of Solid Materials (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Shaping Of Tube Ends By Bending Or Straightening (AREA)
  • Fuel Cell (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Production Of Liquid Hydrocarbon Mixture For Refining Petroleum (AREA)
US09/214,951 1996-07-23 1997-07-23 Furnace having toroidal fluid flow heating zone Expired - Lifetime US6139313A (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
GB9615425 1996-07-23
GB9615418 1996-07-23
GB9615425A GB2315432B (en) 1996-07-23 1996-07-23 Furnaces
GB9615418A GB2315431B (en) 1996-07-23 1996-07-23 Furnaces
PCT/GB1997/002000 WO1998003256A1 (en) 1996-07-23 1997-07-23 Furnace having toroidal fluid flow heating zone

Publications (1)

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US6139313A true US6139313A (en) 2000-10-31

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US09/214,951 Expired - Lifetime US6139313A (en) 1996-07-23 1997-07-23 Furnace having toroidal fluid flow heating zone

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US (1) US6139313A (da)
EP (1) EP0914201B1 (da)
JP (1) JP4115533B2 (da)
AT (1) ATE206071T1 (da)
AU (1) AU730499B2 (da)
BR (1) BR9710516A (da)
CA (1) CA2261230C (da)
DE (1) DE69706993T2 (da)
DK (1) DK0914201T3 (da)
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Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040129177A1 (en) * 2001-02-20 2004-07-08 Gael Cadoret Method and installation for the dehydroxylation treatment of aluminium silicate
US20080264295A1 (en) * 2005-02-09 2008-10-30 Imerys Minerals Limited Treatment of Metakaolin
WO2009129977A1 (en) * 2008-04-24 2009-10-29 Outotec Oyj Process and plant for the heat treatment of fine-grained mineral solids
US20100167921A1 (en) * 2006-09-06 2010-07-01 World Minerals, Inc. Process for Roasting Diatomaceous Earth Ore to Reduce Organic Content
DE112008002943T5 (de) 2007-10-30 2010-09-09 World Minerals Inc., Santa Barbara Modifizierte mineral-basierte Füllstoffe
US20110174732A1 (en) * 2008-09-26 2011-07-21 World Minerals, Inc. Diatomaceous earth products containing reduced soluble metal levels, processes for reducing soluble metal levels in diatomaceous earth products, and methods of using the same
US20130220790A1 (en) * 2010-11-30 2013-08-29 Mortimer Technology Holdings Limited Toroidal bed reactor
CN109502596A (zh) * 2018-12-29 2019-03-22 中国矿业大学 一种速降闪煅高岭土制备偏高岭土的方法

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB9723818D0 (en) 1997-11-12 1998-01-07 Ecc Int Ltd Porous inorganic particulate material

Citations (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3889393A (en) * 1973-04-05 1975-06-17 Kloeckner Humboldt Deutz Ag Device for thermically treating granular and/or lumpy materials
FR2262776A1 (da) * 1974-02-28 1975-09-26 Zjednoczenie Przemyslu Ceramik
US4025293A (en) * 1975-10-14 1977-05-24 Karl Beckenbach Process and apparatus for firing and sintering of granular material
US4076493A (en) * 1976-09-09 1978-02-28 Kennedy Van Saun Corporation Apparatus for cooling particulate material
EP0068853A2 (en) * 1981-06-29 1983-01-05 Torftech Limited Method and apparatus for processing matter in a turbulent mass of particulate material
GB2119279A (en) * 1982-04-26 1983-11-16 Okawara Mfg Gas distributing floor for a circulating fluidized-bed dryer incinerator or the like
EP0172530A2 (de) * 1984-08-20 1986-02-26 Herbert Hüttlin Fliessbettapparatur
GB2203670A (en) * 1987-04-10 1988-10-26 Torftech Ltd Process on or with liquid
GB2219521A (en) * 1988-06-08 1989-12-13 Torftech Ltd Heating matter
WO1992002289A1 (en) * 1990-08-03 1992-02-20 Comalco Aluminium Limited Gas-solide contacting method
WO1992021439A1 (de) * 1991-06-05 1992-12-10 Huettlin Herbert Fliessbettapparatur zum behandeln partikelförmigen gutes
WO1994019122A1 (en) * 1993-02-24 1994-09-01 Great Eastern (Bermuda), Ltd. Process and apparatus for removal of petroleum from particulate materials
WO1995017982A1 (en) * 1993-12-24 1995-07-06 Torftech Limited Contaminant removal

Patent Citations (14)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3889393A (en) * 1973-04-05 1975-06-17 Kloeckner Humboldt Deutz Ag Device for thermically treating granular and/or lumpy materials
FR2262776A1 (da) * 1974-02-28 1975-09-26 Zjednoczenie Przemyslu Ceramik
US4025293A (en) * 1975-10-14 1977-05-24 Karl Beckenbach Process and apparatus for firing and sintering of granular material
US4076493A (en) * 1976-09-09 1978-02-28 Kennedy Van Saun Corporation Apparatus for cooling particulate material
US4559719A (en) * 1981-06-29 1985-12-24 Torftech Limited Method for processing matter in a turbulent mass of particulate material
EP0068853A2 (en) * 1981-06-29 1983-01-05 Torftech Limited Method and apparatus for processing matter in a turbulent mass of particulate material
GB2119279A (en) * 1982-04-26 1983-11-16 Okawara Mfg Gas distributing floor for a circulating fluidized-bed dryer incinerator or the like
EP0172530A2 (de) * 1984-08-20 1986-02-26 Herbert Hüttlin Fliessbettapparatur
GB2203670A (en) * 1987-04-10 1988-10-26 Torftech Ltd Process on or with liquid
GB2219521A (en) * 1988-06-08 1989-12-13 Torftech Ltd Heating matter
WO1992002289A1 (en) * 1990-08-03 1992-02-20 Comalco Aluminium Limited Gas-solide contacting method
WO1992021439A1 (de) * 1991-06-05 1992-12-10 Huettlin Herbert Fliessbettapparatur zum behandeln partikelförmigen gutes
WO1994019122A1 (en) * 1993-02-24 1994-09-01 Great Eastern (Bermuda), Ltd. Process and apparatus for removal of petroleum from particulate materials
WO1995017982A1 (en) * 1993-12-24 1995-07-06 Torftech Limited Contaminant removal

Cited By (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20040129177A1 (en) * 2001-02-20 2004-07-08 Gael Cadoret Method and installation for the dehydroxylation treatment of aluminium silicate
BG65259B1 (bg) * 2001-02-20 2007-10-31 Saint-Gobain Materiaux De Construction Метод и инсталация за дехидроксилиране на алуминиев силикат
US20080264295A1 (en) * 2005-02-09 2008-10-30 Imerys Minerals Limited Treatment of Metakaolin
US20100167921A1 (en) * 2006-09-06 2010-07-01 World Minerals, Inc. Process for Roasting Diatomaceous Earth Ore to Reduce Organic Content
US9943079B2 (en) 2007-10-30 2018-04-17 Imerys Filtration Minerals, Inc. Modified mineral-based fillers
DE112008002943T5 (de) 2007-10-30 2010-09-09 World Minerals Inc., Santa Barbara Modifizierte mineral-basierte Füllstoffe
US20100260866A1 (en) * 2007-10-30 2010-10-14 World Minerals, Inc. Modified mineral-based fillers
US20110034318A1 (en) * 2008-04-24 2011-02-10 Outotec Oyj Process and plant for the heat treatment of fine-grained mineral solids
GB2471256A (en) * 2008-04-24 2010-12-22 Outotec Oyj Process and plant for the heat treatment of fine-grained mineral solids
GB2471256B (en) * 2008-04-24 2012-08-01 Outotec Oyj Process and plant for the heat treatment of fine-grained mineral solids
WO2009129977A1 (en) * 2008-04-24 2009-10-29 Outotec Oyj Process and plant for the heat treatment of fine-grained mineral solids
US20110174732A1 (en) * 2008-09-26 2011-07-21 World Minerals, Inc. Diatomaceous earth products containing reduced soluble metal levels, processes for reducing soluble metal levels in diatomaceous earth products, and methods of using the same
US8663475B2 (en) 2008-09-26 2014-03-04 Imerys Filtration Minerals, Inc. Diatomaceous earth products containing reduced soluble metal levels, processes for reducing soluble metal levels in diatomaceous earth products, and methods of using the same
US20130220790A1 (en) * 2010-11-30 2013-08-29 Mortimer Technology Holdings Limited Toroidal bed reactor
US10245573B2 (en) * 2010-11-30 2019-04-02 Mortimer Technology Holdings Limited Toroidal bed reactor
CN109502596A (zh) * 2018-12-29 2019-03-22 中国矿业大学 一种速降闪煅高岭土制备偏高岭土的方法

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DE69706993D1 (de) 2001-10-31
JP4115533B2 (ja) 2008-07-09
AU730499B2 (en) 2001-03-08
DK0914201T3 (da) 2002-01-28
EP0914201B1 (en) 2001-09-26
ES2164360T3 (es) 2002-02-16
CA2261230A1 (en) 1998-01-29
CA2261230C (en) 2008-09-23
JP2000515234A (ja) 2000-11-14
BR9710516A (pt) 2000-01-11
WO1998003256A1 (en) 1998-01-29
DE69706993T2 (de) 2002-04-04
AU3630697A (en) 1998-02-10
ATE206071T1 (de) 2001-10-15
PT914201E (pt) 2002-03-28
EP0914201A1 (en) 1999-05-12

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